Liquid-liquid extraction based on reversible chemical complexation is a nov
el separation technique that is highly effective and selective for separati
ng polar organic solutes from aqueous solutions. Equilibria of aqueous solu
tions of formic acid, acetic acid, propionic acid, butyric acid, caproic ac
id, monochloroacetic acid, dichloroacetic acid, trichloroacetic acid, and l
actic acid with trialkylphosphine oxide in kerosene were investigated. Equi
librium concentrations are given at 298 K. An extraction equilibrium model
was used to describe the experimental data. Calculated organic acid concent
rations in both phases are in good agreement with the experimental values.